EP0162015B1 - Verfahren zur Herstellung von Indolinen - Google Patents

Verfahren zur Herstellung von Indolinen Download PDF

Info

Publication number
EP0162015B1
EP0162015B1 EP85810220A EP85810220A EP0162015B1 EP 0162015 B1 EP0162015 B1 EP 0162015B1 EP 85810220 A EP85810220 A EP 85810220A EP 85810220 A EP85810220 A EP 85810220A EP 0162015 B1 EP0162015 B1 EP 0162015B1
Authority
EP
European Patent Office
Prior art keywords
aminophenyl
ethanol
process according
catalyst
reaction
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
EP85810220A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0162015A3 (en
EP0162015A2 (de
Inventor
Milos Rusek
Hermann Dr. Kny
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Syngenta Participations AG
Original Assignee
Ciba Geigy AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ciba Geigy AG filed Critical Ciba Geigy AG
Priority to AT85810220T priority Critical patent/ATE70052T1/de
Publication of EP0162015A2 publication Critical patent/EP0162015A2/de
Publication of EP0162015A3 publication Critical patent/EP0162015A3/de
Application granted granted Critical
Publication of EP0162015B1 publication Critical patent/EP0162015B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D209/00Heterocyclic compounds containing five-membered rings, condensed with other rings, with one nitrogen atom as the only ring hetero atom
    • C07D209/02Heterocyclic compounds containing five-membered rings, condensed with other rings, with one nitrogen atom as the only ring hetero atom condensed with one carbocyclic ring
    • C07D209/04Indoles; Hydrogenated indoles
    • C07D209/08Indoles; Hydrogenated indoles with only hydrogen atoms or radicals containing only hydrogen and carbon atoms, directly attached to carbon atoms of the hetero ring

Definitions

  • the present invention relates to a process for the preparation of indolines of the formula I, wherein R1 is hydrogen or C1-C4-alkyl, R2 and R3 are each independently hydrogen, C1 ⁇ 4-alkyl or phenyl, by catalytic cyclodehydration of a 2- (2'-aminophenyl) ethanol of the formula II, in which R1, R2 and R3 have the above meaning, in the gas phase.
  • the indolines of the formula I are intermediates for the preparation of pyrrolo [3,2,1-i, j] quinolines with bactericidal and fungicidal properties which can be used to combat plant diseases.
  • pyrrolo [3,2,1-i, j] quinolines are in British Patents 1,394,373 and 1,394,374.
  • 4-Lilolidone (1,2,5,6-tetrahydro-4H-pyrrolo- [3,2,1-i, j] -quinolin-2-one) of the formula III is particularly representative of this class of substances mentioned.
  • German patent 606 027 it is known to produce indoline in such a way that 2- (2'-aminophenyl) ethanol is heated to 150-500 ° C., in particular 200-400 ° C., in the presence of a condensing agent.
  • the oxides of aluminum, titanium, zirconium, chromium, thor or mixtures of these oxides are mentioned as examples of condensing agents.
  • other compounds such as sulfates, phosphates, silicates, hydrosilicates, borates, chlorides, mineral acids, and acid anhydrides can either be used instead of the aforementioned oxides or in a mixture with them as condensing agents.
  • indolines can be obtained in good yield by the abovementioned processes, these processes are unsuitable for industrial production of indolines because of the rapid deactivation of the catalysts used and because of the effort associated with the regeneration of the catalysts.
  • the indolines of the formula I can be prepared in excellent yield by cyclodehydrating a 2- (2'-aminophenyl) ethanol of the formula II in the gas phase if the cyclodehydration of a 2- (2'-aminophenyl) -ethanol of formula II at 200-350 ° C in the presence of a silicate or an aluminosilicate of an alkaline earth metal or a rare earth metal and in the presence of carrier gas.
  • the preferred temperature range for carrying out the reaction is 240-260 ° C. Because of the endothermic nature of the cyclodehydration according to the invention, heat must be added to the system to maintain the reaction temperature.
  • the cyclodehydration can be carried out under atmospheric or reduced pressure. It is preferred to work under atmospheric pressure.
  • the cyclodehydration is carried out in the presence of carrier gas.
  • carrier gas The use of hydrogen, nitrogen, carbonic acid or water vapor as the carrier gas is possible.
  • the preferred water vapor as the carrier gas can be used in a ratio of 0.2 to 10 moles per mole of 2- (2'-aminophenyl) ethanol.
  • the use of 3 to 5 moles of water vapor per mole of 2- (2'-aminophenyl) ethanol is particularly preferred.
  • Water can be added via separate water or steam lines or by leading the correspondingly concentrated aqueous solution of 2- (2'-aminophenyl) ethanol into the reactor via an evaporator.
  • the alkaline earth metal silicate catalysts which can be used for the cyclodehydration according to the invention can be reacted with an alkali water glass dissolved in water, e.g. Potash water glass with the aqueous solution of an alkaline earth metal salt, e.g. Magnesium nitrate, by filtering, washing and drying the resulting and precipitated alkaline earth metal silicate and by activating it by air passage at temperatures of 300 to 550 ° C.
  • an alkali water glass dissolved in water e.g. Potash water glass
  • an alkaline earth metal salt e.g. Magnesium nitrate
  • the preferred temperature range for the activation of the alkaline earth silicate catalysts is 340-360 ° C.
  • the magnesium silicate is preferably used.
  • Suitable catalysts for the cyclodehydration according to the invention are the synthetic or natural molecular sieves belonging to the group of silicates or aluminosilicates.
  • Such molecular sieves with cations of alkaline earth or rare earth metals can be produced from the synthetic molecular sieves containing alkali metal cations by ion exchange, as described in company documents. (Eg: "Linde Molecular Sieves, Catalyst Bulletin, Union Carbide", 270 Park Ave., New York, NY 10017, USA).
  • catalysts which mainly contain cations of rare earth metals, are also preferred as catalysts. Such catalysts are commercially available.
  • the catalyst offered under the name Strem 14-8910 is, for example, an alumino-silicate molecular sieve enriched with rare earths with the following composition: SiO2 65.0% Al2O3 22.7% Na2O 1.6% Re2O3 10.7%, where Re means the sum of all cations of rare earth metals.
  • moving bed reactors e.g. a fluidized bed reactor or fixed bed reactors are used.
  • the activation or reactivation of the catalyst can take place in one of the reactors mentioned, in parallel with the reaction or alternately therewith.
  • the method according to the invention is suitable for continuous process control.
  • the inventive method is generally applicable for the preparation of the indolines of the formula I, wherein R1 is hydrogen or C1-C4-alkyl, R2 and R3 are each independently hydrogen, C1 Wasserstoff-alkyl or phenyl.
  • C1-C4-alkyl includes methyl, ethyl, n-propyl, isopropyl, primary and secondary n-butyl, isobutyl and tert-butyl.
  • the 2- (2'-aminophenyl) ethanol is in the presence of Mg silicate and with the addition of 3-5 moles of water vapor per mole of 2- (2'-aminophenyl) ethanol at 240- Cyclodehydrated 260 ° to indoline.
  • the substituted 2- (2'-aminophenyl) ethanols used for the cyclodehydration according to the invention can be prepared by reducing the corresponding nitro compounds.
  • the 2- (2'-aminophenyl) ethanol is also readily available from the 2- (2'-nitrophenyl) ethanol by reduction with zinc according to Sabetay (Bull. Soc. Chim. Fr. 1931, 49 3).
  • the 2- (2'-nitrophenyl) ethanol and its substituted derivatives can be obtained by adding o-nitroalkylbenzenes to an aldehyde according to Japanese Patent 77-108941; CA Vol. 88 (1978) 104875x can be produced according to the following reaction scheme:
  • indolines can be prepared by catalytic cyclodehydration of 2- (2'-aminophenyl) ethanols with a selectivity of more than 97% with a conversion of at least 98%, the life of the catalyst advantageously being compared to the processes known hitherto is extended many times. According to the invention, this advantageous effect is achieved by adding carrier gas.
  • 3 ml of the catalyst thus prepared are placed in the catalyst bed of a microreactor. 3 ml / hour of a 65% aqueous solution of 2- (2'-aminophenyl) ethanol are metered into the reactor at atmospheric pressure. The temperature of the catalyst is kept at 260 ° C.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Indole Compounds (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Catalysts (AREA)
EP85810220A 1984-05-16 1985-05-09 Verfahren zur Herstellung von Indolinen Expired - Lifetime EP0162015B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT85810220T ATE70052T1 (de) 1984-05-16 1985-05-09 Verfahren zur herstellung von indolinen.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US61072784A 1984-05-16 1984-05-16
US610727 1996-03-04

Publications (3)

Publication Number Publication Date
EP0162015A2 EP0162015A2 (de) 1985-11-21
EP0162015A3 EP0162015A3 (en) 1988-07-06
EP0162015B1 true EP0162015B1 (de) 1991-12-04

Family

ID=24446177

Family Applications (1)

Application Number Title Priority Date Filing Date
EP85810220A Expired - Lifetime EP0162015B1 (de) 1984-05-16 1985-05-09 Verfahren zur Herstellung von Indolinen

Country Status (6)

Country Link
EP (1) EP0162015B1 (xx)
JP (1) JPS60246366A (xx)
KR (1) KR920001464B1 (xx)
AT (1) ATE70052T1 (xx)
DE (1) DE3584791D1 (xx)
ZA (1) ZA853689B (xx)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4886887A (en) * 1985-11-08 1989-12-12 Ciba-Geigy Corporation Process for the preparation of indolines
JPS63196561A (ja) * 1987-02-07 1988-08-15 Idemitsu Kosan Co Ltd インド−ル類の製造方法

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE606027C (de) * 1933-11-16 1934-11-23 I G Farbenindustrie Akt Ges Verfahren zur Herstellung von Indolinen und Indolen
JPS52108969A (en) * 1976-03-09 1977-09-12 Mitsui Petrochem Ind Ltd Preparation of indolines
JPS52142063A (en) * 1976-05-19 1977-11-26 Mitsui Petrochem Ind Ltd Preparation of indoles
HU177029B (hu) * 1979-05-29 1981-06-28 Reanal Finomvegyszergyar Sposob poluchenija indola,1,283,4-tetragidrokhinolina i ikh proizvodnykh
JPS5835171A (ja) * 1981-08-25 1983-03-01 Mitsui Toatsu Chem Inc インド−ルの改良された製造方法

Also Published As

Publication number Publication date
ZA853689B (en) 1985-12-24
ATE70052T1 (de) 1991-12-15
JPS60246366A (ja) 1985-12-06
DE3584791D1 (de) 1992-01-16
EP0162015A3 (en) 1988-07-06
KR920001464B1 (ko) 1992-02-14
KR850008338A (ko) 1985-12-16
JPH0471909B2 (xx) 1992-11-16
EP0162015A2 (de) 1985-11-21

Similar Documents

Publication Publication Date Title
EP0170182B1 (de) Verfahren zur Gewinnung von 2-Butenen aus 1-Buten und gegebenenfalls 2-Butene enthaltenden C4-Kohlenwasserstoffgemischen
DE2321399C2 (de) Verfahren zur Alkylierung von aromatischen Kohlenwasserstoffen
US4804758A (en) Preparation of 1,4-diazabicyclo[2.2.2]octanes
EP0332075B1 (de) Verfahren zur Herstellung von acylierten Imidazolen
EP0162015B1 (de) Verfahren zur Herstellung von Indolinen
EP0267438B1 (de) Verfahren zur Herstellung von ungesättigten Nitrilen
EP0206143A1 (de) Verfahren zur Herstellung von 4-Pentensäureestern
EP0295552B1 (de) Verfahren zur Herstellung von Pentensäureestern
EP0232712A1 (de) Verfahren zur Herstellung von Nitrilen
EP0196554A1 (de) Verfahren zur Herstellung von aliphatischen Dinitrilen
US4904806A (en) Preparation of tetrahydrofurans from butane-1,4-diols
EP0167021B1 (de) Verfahren zur Herstellung von 2-Methyl-2-alkenalen
US4694107A (en) Preparation of ketones by isomerization of aldehydes
AT201579B (de) Verfahren zur Herstellung von Acrylsäure
EP0190101B1 (de) Verfahren zur Herstellung von N-Alkylanilinen
EP0168761B1 (de) Verfahren zur Herstellung von 2-Methyl-2-alkenalen aus Dihydropyranen
EP0290862A2 (de) Verfahren zur Herstellung von 1,4-Diazabicyclo(2,2,2)-octanen
EP0444460A2 (de) Verfahren zur Herstellung von Acrolein
EP0306875A2 (de) Verfahren zur Herstellung von 5-Methylbutyrolacton
EP0269043B1 (de) Verfahren zur Herstellung von 3-Pentensäureestern aus 2-Pentensäureestern
EP0300324A1 (de) Verfahren zur Herstellung von acylierten Imidazolen und Pyrazolen
EP0289924A2 (de) Verfahren zur Herstellung von Pyridinen
HU200154B (en) Process for producing dien-1-ols
DE3634257A1 (de) Verfahren zur herstellung von 1,4- diazabicyclo(2,2,2)-octanen
EP0132737A2 (de) Verfahren zur Isomerisierung von Diacyloxy-butenen

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 19850511

AK Designated contracting states

Designated state(s): AT BE CH DE FR GB IT LI NL SE

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AT BE CH DE FR GB IT LI NL SE

17Q First examination report despatched

Effective date: 19900808

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

ITF It: translation for a ep patent filed
AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH DE FR GB IT LI NL SE

REF Corresponds to:

Ref document number: 70052

Country of ref document: AT

Date of ref document: 19911215

Kind code of ref document: T

REF Corresponds to:

Ref document number: 3584791

Country of ref document: DE

Date of ref document: 19920116

ET Fr: translation filed
GBT Gb: translation of ep patent filed (gb section 77(6)(a)/1977)
PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
EAL Se: european patent in force in sweden

Ref document number: 85810220.5

REG Reference to a national code

Ref country code: CH

Ref legal event code: PFA

Free format text: CIBA-GEIGY AG TRANSFER- NOVARTIS AG

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

NLS Nl: assignments of ep-patents

Owner name: NOVARTIS AG

REG Reference to a national code

Ref country code: FR

Ref legal event code: TP

REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

REG Reference to a national code

Ref country code: CH

Ref legal event code: PUE

Owner name: SYNGENTA PARTICIPATIONS AG

Free format text: NOVARTIS AG#SCHWARZWALDALLEE 215#4058 BASEL (CH) -TRANSFER TO- SYNGENTA PARTICIPATIONS AG#SCHWARZWALDALLEE 215#4058 BASEL (CH)

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: SE

Payment date: 20030507

Year of fee payment: 19

Ref country code: GB

Payment date: 20030507

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20030508

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 20030514

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 20030516

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20030522

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20030530

Year of fee payment: 19

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20030725

Year of fee payment: 19

NLS Nl: assignments of ep-patents

Owner name: SYNGENTA PARTICIPATIONS AG

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040509

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040509

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040510

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040531

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040531

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20040531

BERE Be: lapsed

Owner name: *SYNGENTA PARTICIPATIONS A.G.

Effective date: 20040531

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20041201

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20041201

EUG Se: european patent has lapsed
GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20040509

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20050131

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 20041201

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

REG Reference to a national code

Ref country code: FR

Ref legal event code: TP